US4397834A - Method of gettering hydrogen under conditions of low pressure - Google Patents
Method of gettering hydrogen under conditions of low pressure Download PDFInfo
- Publication number
- US4397834A US4397834A US06/337,339 US33733982A US4397834A US 4397834 A US4397834 A US 4397834A US 33733982 A US33733982 A US 33733982A US 4397834 A US4397834 A US 4397834A
- Authority
- US
- United States
- Prior art keywords
- hydrogen
- compound
- gettering
- pressure
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/0005—Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes
- C01B3/001—Reversible uptake of hydrogen by an appropriate medium, i.e. based on physical or chemical sorption phenomena or on reversible chemical reactions, e.g. for hydrogen storage purposes ; Reversible gettering of hydrogen; Reversible uptake of hydrogen by electrodes characterised by the uptaking medium; Treatment thereof
- C01B3/0031—Intermetallic compounds; Metal alloys; Treatment thereof
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S420/00—Alloys or metallic compositions
- Y10S420/90—Hydrogen storage
Definitions
- the invention relates to a ternary intermetallic-compound capable of reversibly sorbing hydrogen. More specifically, this invention relates to a ternary intermetallic-compound capable of gettering hydrogen at low pressures and at temperatures from about room to about 200° C. and which can be regenerated at low pressures and at temperatures from about 300°-500° C.
- the temperature and pressure ranges at which gettering and regeneration can occur can be controlled by varying the composition of the compound.
- impurities in the plasma of magnetic confinement fusion devices such as Tokamaks can seriously limit the performance of such devices by lowering the plasma temperature and quenching the fusion reaction.
- impurities are introduced into the plasma by a variety of sputtering and erosion processes occuring at the walls of the devices by hydrogen isotope recycling.
- These impurities may consist of oxygen, carbon and hydrogen, including the isotopes deuterium and tritium
- Some metal ions may also be included which have been sputtered from the wall of the device during operation.
- Some solutions to the problem of impurity control include modifying the recycling processes, minimizing the erosion rates at the surfaces facing the plasma and removing the offending impurities from the plasma. It has been shown that the trapping and subsequent re-admission of hydrogen isotopes from walls affects plasma profiles, especially at the edge, substantially modifying impurity influxes. In deuterium-tritium burning devices, wall recycling will strongly influence tritium inventory, which must be held to within well-defined limits. Therefore, tritium retention is an important factor in the design of a suitable fusion device.
- the material which can getter hydrogen and hydrogen isotopes under the low pressure, high temperature conditions present in operating magnetic containment fusion devices. Furthermore, the material must be capable of being regenerated for recycling under reasonable condition of pressure and temperature.
- a material can be placed in the fusion device either as a coating on the walls of the device or as a coating on sheets of substrate which can be placed within the device.
- the material is reasonably selective for hydrogen, must be able to function as a hydrogen and hydrogen isotope getter at pressures down to at least 10 -6 torr, in the presence of power fluxes up to about 50 w/cm 2 and at temperatures from about room temperature up to about 200° C.
- the material should have a high hydrogen capacity in order to reduce the frequency of regeneration, it should be able to be regenerated with respect to absorbed hydrogen at a relatively low temperature, preferably no higher than 500° C., and it must be able to function as a hydrogen getter in the presence of other contaminant gases, such as CO, O 2 and N 2 .
- chromium for some of the vanadium in a zirconium-vanadium alloy will form a ternary intermetallic-compound, which is useful as a hydrogen getter under the vacuum and temperature environment found within most magnetic fusion devices. Furthermore, the alloy can be regenerated under vacuum conditions at temperatures as low as about 300° C.
- the ternary intermetallic compound has the formula Zr(V 1-x Cr x ) 2 where x is in the range of 0.01 to 0.90.
- FIG. 1 contains several curves showing hydrogen absorption isotherms for the compound Zr(V 0 .4 Cr 0 .6) 2 at several different temperatures.
- FIG. 3 contains several curves showing the relationship between gettering pressure and temperature.
- the compound is prepared by melting together appropriate quantities of high-purity powder of zirconium, vanadium and chromium, in a furnace under an inert atmosphere, to form the compound. Preferably, each powdered mixture is melted together several times in order to ensure complete homogeniety of the alloy.
- the homogenized intermetallic compound must be activated before it can be successfully used as a hydrogen getter. This is accomplished by contacting the compound with hydrogen gas at a pressure at least above the decomposition pressure of the compound, generally at least one to two atmospheres, for a period of time sufficient to hydride the compounds, generally from 1/2 to 2 hours. It may be preferred to granulate the material to 1/4 to 1/2 inch particles to ensure complete activation.
- the amount of chromium in the alloy may vary from about 0.01 to about 0.9 mols.
- An increase of chromium in the alloy will lower the temperature at which gettering will take place at a given pressure and will also lower the hydrogen capacity of the alloy.
- the exact amount of chromium desired in an alloy will depend upon the pressure and temperature conditions under which hydrogen gettering is to take place and perhaps more importantly, on the pressure and temperature conditions which are available to regenerate the getter.
- An intermetallic compound having the formula Zr(V 0 .4 Cr 0 .6) 2 was prepared by placing a charge containing the appropriate quantities of 99.9% purity powdered materials into water-cooled copper crucible. The charge was melted three times at 100 amps with a tungsten electrode under an argon atmosphere.
- 1.0104 gm of the sample was then placed in a quartz tube and connected to an all metal vacuum line.
- the sample was activated at room temperature with a hydrogen pressure of 27 psia. After the initial hydrogen absorption, the hydrogen was then removed by pumping on the sample at 700° C.
- An adsorption isotherm for the sample at 450° C. was prepared by heating the sample to that temperature, adding about 10 Torr-liters of H 2 to the alloy and waiting 10 to 60 minutes for the pressure to equilibrate. After equilibration, the pressure was noted and another aliquot of about 10 Torr-liters of hydrogen gas was added to the tube and the pressure equilibrated again.
- Example II Additional samples of the ternary intermetallic compound having the formula Zr(V 0 .5 Cr 0 .5) 2 and Zr(V 0 .6 Cr 0 .4) 2 were prepared and activated as described in Example I. A hydrogen absorption isotherm for the samples at 450° C. was then prepared. The results are shown in FIG. 2. For comparison, the isotherm for Zr(V 0 .4 Cr 0 .6) 2 at 450° C. taken from FIG. 1 is also shown.
- a 0.2558 gm sample of a hydrided alloy of the composition Zr(V 0 .6 Cr 0 .4) 2 H x was weighted into one chamber of a quartz tube having two chambers.
- the tube was connected to a high vacuum system.
- the sample was heated to about 500° C. and degassed at a pressure of 8 ⁇ 10 -7 Torr.
- the getter was then cooled and maintained at a temperature of about 200° C.
- the vessel containing the getter was valved off and a pressure of 2.6 ⁇ 10 -2 Torr of hydrogen gas was admitted to the main chamber of the quartz tube.
- the getter was then exposed to the hydrogen gas.
- the system pressure dropped to about 3 ⁇ 10 -5 Torr, confirming the capability of the material to getter hydrogen at low pressures and temperatures of 200° C.
- the hydrided alloy of Example III was regenerated by heating to about 500° C. and pumping to a pressure of about 7 ⁇ 10 -7 Torr which removed most of the hydrogen gas absorbed in the previous example.
- the getter was cooled to about 200° C. and isolated from the main chamber. Hydrogen gas was again added to the main chamber, which had a volume of about 1 liter, at a pressure of 3.3 ⁇ 10 -2 Torr. When the valve to the getter chamber was opened, the system pressure dropped to 3 ⁇ 10 -5 Torr within one minute. It was determined that the getter absorbed about 0.03 Torr-liters of hydrogen gas.
- FIG. 3 which contains several curves showing the relationship between gettering pressure and temperature for several compounds of the invention was derived from FIGS. 1 and 2 in the following manner.
- the pressures at three temperatures 450°, 400° and 350° C.
- the presures at 450° C. at the hydrogen composition of 20 Torr-liters H 2 absorbed/gm alloy were taken from FIG. 2 After assuming the thermodynamic entropies to be equal for all three compounds, the lines shown in FIG. 3 were drawn.
- the compound Zr(V 0 .6 Cr 0 .4) 2 has a minimum hydrogen partial pressure which can be gettered of about 5 ⁇ 10 -6 Torr (about 6.2 ⁇ 10 -9 atm), while Zr(V 0 .5 Cr 0 .5) 2 has a pressure of about 5 ⁇ 10 -8 atm.
- the minimum hydrogen partial pressure which can be gettered increases as the proportion of chromium in the gettering compound increases.
- the gettering temperature decreases. It is clear from the diagram that a gettering compound can be specifically formulated for the temperature and pressure requirements of a particular gettering environment by preselecting the proportions of vanadium and chromium in the compound.
- the regeneration temperature is a complex function of the system pumping speed, the regeneration time allowed, and the extent of regeneration required, i.e. how much hydrogen must be removed.
- any temperature over 200° C. will cause some amount of regeneration, that is to say decomposition of the hydride to alloy hydrogen gas.
- the highest permissible regeneration temperature should be used to effect the most complete and most rapid regeneration.
- the ternary metallic compound of the invention is capable of gettering hydrogen at pressures down to 10 -7 Torr at temperatures varying from about room up to about 200° C. and furthermore that the compound can be regenerated for recycle at temperatures varying from 300° to 500° C.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
A ternary intermetallic compound having the formula Zr(V1-x Crx)2 where x is in the range of 0.01 to 0.90 is capable of reversibly sorbing hydrogen at temperatures ranging from room temperature to 200° C., at pressures down to 10-6 Torr. The compound is suitable for use as a hydrogen getter in low pressure, high temperature applications such as magnetic confinement fusion devices.
Description
The United States Government has rights in this invention pursuant to Contract No. W-31-109-ENG-38 between the U.S. Department of Energy and Argonne National Laboratory.
This is a division of application Ser. No. 196,710, filed Oct. 14, 1980 now abandoned.
The invention relates to a ternary intermetallic-compound capable of reversibly sorbing hydrogen. More specifically, this invention relates to a ternary intermetallic-compound capable of gettering hydrogen at low pressures and at temperatures from about room to about 200° C. and which can be regenerated at low pressures and at temperatures from about 300°-500° C. The temperature and pressure ranges at which gettering and regeneration can occur can be controlled by varying the composition of the compound.
It is generally recognized that impurities in the plasma of magnetic confinement fusion devices such as Tokamaks can seriously limit the performance of such devices by lowering the plasma temperature and quenching the fusion reaction. These impurities are introduced into the plasma by a variety of sputtering and erosion processes occuring at the walls of the devices by hydrogen isotope recycling. These impurities may consist of oxygen, carbon and hydrogen, including the isotopes deuterium and tritium Some metal ions may also be included which have been sputtered from the wall of the device during operation.
Some solutions to the problem of impurity control include modifying the recycling processes, minimizing the erosion rates at the surfaces facing the plasma and removing the offending impurities from the plasma. It has been shown that the trapping and subsequent re-admission of hydrogen isotopes from walls affects plasma profiles, especially at the edge, substantially modifying impurity influxes. In deuterium-tritium burning devices, wall recycling will strongly influence tritium inventory, which must be held to within well-defined limits. Therefore, tritium retention is an important factor in the design of a suitable fusion device.
There is need for a material which can getter hydrogen and hydrogen isotopes under the low pressure, high temperature conditions present in operating magnetic containment fusion devices. Furthermore, the material must be capable of being regenerated for recycling under reasonable condition of pressure and temperature. Such a material can be placed in the fusion device either as a coating on the walls of the device or as a coating on sheets of substrate which can be placed within the device. Preferably the material is reasonably selective for hydrogen, must be able to function as a hydrogen and hydrogen isotope getter at pressures down to at least 10-6 torr, in the presence of power fluxes up to about 50 w/cm2 and at temperatures from about room temperature up to about 200° C. Furthermore, the material should have a high hydrogen capacity in order to reduce the frequency of regeneration, it should be able to be regenerated with respect to absorbed hydrogen at a relatively low temperature, preferably no higher than 500° C., and it must be able to function as a hydrogen getter in the presence of other contaminant gases, such as CO, O2 and N2.
One such material which has been used successfully is sublimed titanium. However, titanium is not easily regenerated and fresh layers of titanium must be sublimed for each gettering cycle that is required, which is expensive and time consuming. Another material which fulfills many of the requirements is ST101®. This material is a proprietary Zr-Al based alloy available from SAES Getters of Milan, Italy. However, hydrogen capacity of the alloy is somewhat limited and regeneration of the alloy within a reasonable length of time requires that it be heated to temperatures of at least 750° C.
It has been found that the substitution of chromium for some of the vanadium in a zirconium-vanadium alloy will form a ternary intermetallic-compound, which is useful as a hydrogen getter under the vacuum and temperature environment found within most magnetic fusion devices. Furthermore, the alloy can be regenerated under vacuum conditions at temperatures as low as about 300° C. The ternary intermetallic compound has the formula Zr(V1-x Crx)2 where x is in the range of 0.01 to 0.90. By varying the amount of chromium present in the alloy, it is possible to control the pressure and temperature conditions under which the compound will getter hydrogen and most important the conditions under which the getter can be regenerated. This allows the chemical properties of the compound of the invention to be tailored to fit the operating and regeneration requirements in terms of pressure and temperature of different fusion devices.
It is therefore one object of the invention to provide a material which is suitable for use as a hydrogen getter in a fusion plasma type reactor.
It is another object of the invention to provide a ternary intermetallic compound which is capable of gettering hydrogen at temperatures varying from about room temperature to about 200° C. and at pressures down to about 10-6 torr.
It is still another object of the invention to provide a ternary intermetallic compound which is capable of gettering hydrogen at temperatures varying from about room temperature to about 200° C., at pressures down to about 10-6 torr, and which can be regenerated at temperatures from about 300° and 500° C.
Finally, it is the object of the invention to provide a ternary intermetallic compound in which the gettering conditions and the regenerating conditions can be controlled.
FIG. 1 contains several curves showing hydrogen absorption isotherms for the compound Zr(V0.4 Cr0.6)2 at several different temperatures.
FIG. 2 contains several curves showing pressure composition absorption isotherms at 450° C. for the compound Zr(V1-x Cox)2 where x=0.4, 0.5 and 0.6.
FIG. 3 contains several curves showing the relationship between gettering pressure and temperature.
The ternary intermetallic compound of the invention has the formula Zr(V1-x Crx)2 where x=0.01 to 0.90. The compound is prepared by melting together appropriate quantities of high-purity powder of zirconium, vanadium and chromium, in a furnace under an inert atmosphere, to form the compound. Preferably, each powdered mixture is melted together several times in order to ensure complete homogeniety of the alloy.
The homogenized intermetallic compound must be activated before it can be successfully used as a hydrogen getter. This is accomplished by contacting the compound with hydrogen gas at a pressure at least above the decomposition pressure of the compound, generally at least one to two atmospheres, for a period of time sufficient to hydride the compounds, generally from 1/2 to 2 hours. It may be preferred to granulate the material to 1/4 to 1/2 inch particles to ensure complete activation.
The amount of chromium in the alloy may vary from about 0.01 to about 0.9 mols. An increase of chromium in the alloy will lower the temperature at which gettering will take place at a given pressure and will also lower the hydrogen capacity of the alloy. Thus, the exact amount of chromium desired in an alloy will depend upon the pressure and temperature conditions under which hydrogen gettering is to take place and perhaps more importantly, on the pressure and temperature conditions which are available to regenerate the getter.
X-ray diffraction patterns taken of the compound of the invention by the Debye-Scherrer method with filtered Cu radiation, have shown that the crystal structure is of the cubic MgCu2 -type. Lattice expansion on hydriding was found to be about 20% for the compound Zr(V0.4 Cr0.6)2.
An intermetallic compound having the formula Zr(V0.4 Cr0.6)2 was prepared by placing a charge containing the appropriate quantities of 99.9% purity powdered materials into water-cooled copper crucible. The charge was melted three times at 100 amps with a tungsten electrode under an argon atmosphere.
1.0104 gm of the sample was then placed in a quartz tube and connected to an all metal vacuum line. The sample was activated at room temperature with a hydrogen pressure of 27 psia. After the initial hydrogen absorption, the hydrogen was then removed by pumping on the sample at 700° C. An adsorption isotherm for the sample at 450° C. was prepared by heating the sample to that temperature, adding about 10 Torr-liters of H2 to the alloy and waiting 10 to 60 minutes for the pressure to equilibrate. After equilibration, the pressure was noted and another aliquot of about 10 Torr-liters of hydrogen gas was added to the tube and the pressure equilibrated again. This procedure was repeated until a maximum composition of 60-80 Torr-liters of H2 absorbed/gm alloy was reached. In a like manner, hydrogen isotherms for material of the same composition at 400° C. and 350° C. were also determined. The results are shown in FIG. 1.
Additional samples of the ternary intermetallic compound having the formula Zr(V0.5 Cr0.5)2 and Zr(V0.6 Cr0.4)2 were prepared and activated as described in Example I. A hydrogen absorption isotherm for the samples at 450° C. was then prepared. The results are shown in FIG. 2. For comparison, the isotherm for Zr(V0.4 Cr0.6)2 at 450° C. taken from FIG. 1 is also shown.
As a test of the gettering capability of the material, a 0.2558 gm sample of a hydrided alloy of the composition Zr(V0.6 Cr0.4)2 Hx was weighted into one chamber of a quartz tube having two chambers. The tube was connected to a high vacuum system. The sample was heated to about 500° C. and degassed at a pressure of 8×10-7 Torr. The getter was then cooled and maintained at a temperature of about 200° C. The vessel containing the getter was valved off and a pressure of 2.6×10-2 Torr of hydrogen gas was admitted to the main chamber of the quartz tube. The getter was then exposed to the hydrogen gas. Within 1 minute the system pressure dropped to about 3×10-5 Torr, confirming the capability of the material to getter hydrogen at low pressures and temperatures of 200° C.
The hydrided alloy of Example III was regenerated by heating to about 500° C. and pumping to a pressure of about 7×10-7 Torr which removed most of the hydrogen gas absorbed in the previous example. The getter was cooled to about 200° C. and isolated from the main chamber. Hydrogen gas was again added to the main chamber, which had a volume of about 1 liter, at a pressure of 3.3×10-2 Torr. When the valve to the getter chamber was opened, the system pressure dropped to 3×10-5 Torr within one minute. It was determined that the getter absorbed about 0.03 Torr-liters of hydrogen gas.
FIG. 3 which contains several curves showing the relationship between gettering pressure and temperature for several compounds of the invention was derived from FIGS. 1 and 2 in the following manner. For the alloy Zr(V0.4 Cr0.6)2, the pressures at three temperatures (450°, 400° and 350° C.) were taken from FIG. 1 at a hydrogen composition of 20 Torr-liters H2 absorbed/gm alloy and plotted on FIG. 3. To obtain these lines for Zr(V0.5 Cr0.5)2 and Zr(V0.6 Cr0.4)2, the presures at 450° C. at the hydrogen composition of 20 Torr-liters H2 absorbed/gm alloy were taken from FIG. 2 After assuming the thermodynamic entropies to be equal for all three compounds, the lines shown in FIG. 3 were drawn.
From given operating temperature it is possible using FIG. 3 to determine the minimum hydrogen partial pressure which can be gettered for each compound. Thus for an operating temperature of about 200° C. the compound Zr(V0.6 Cr0.4)2 has a minimum hydrogen partial pressure which can be gettered of about 5×10-6 Torr (about 6.2×10-9 atm), while Zr(V0.5 Cr0.5)2 has a pressure of about 5×10-8 atm. It may further be seen from FIG. 3 that the minimum hydrogen partial pressure which can be gettered increases as the proportion of chromium in the gettering compound increases. In addition, it may be seen that as the proportion of chromium in the gettering compound increases the gettering temperature decreases. It is clear from the diagram that a gettering compound can be specifically formulated for the temperature and pressure requirements of a particular gettering environment by preselecting the proportions of vanadium and chromium in the compound.
The regeneration temperature is a complex function of the system pumping speed, the regeneration time allowed, and the extent of regeneration required, i.e. how much hydrogen must be removed. For Zr(V0.6 Cr0.4)2 any temperature over 200° C. will cause some amount of regeneration, that is to say decomposition of the hydride to alloy hydrogen gas. In general, while any temperature above the operating temperature may be used as a regeneration temperature, the highest permissible regeneration temperature should be used to effect the most complete and most rapid regeneration.
From the preceeding discussion and Examples, it can be seen that the ternary metallic compound of the invention is capable of gettering hydrogen at pressures down to 10-7 Torr at temperatures varying from about room up to about 200° C. and furthermore that the compound can be regenerated for recycle at temperatures varying from 300° to 500° C.
Claims (4)
1. In a method of gettering hydrogen from a low pressure environment comprising contacting the hydrogen at a pressure as low as 10-6 torr with a ternary intermetallic compound, the improvement wherein said compound has the formula Zr(V1-x Crx)2 where 0.01≦x≦0.90, and wherein x is preselected in accordance with the requirements of said gettering environment such that when x is low, the minimum hydrogen gettering pressure is lower and the gettering temperature is higher, and when x is high, the minimum hydrogen gettering pressure is higher and the gettering temperature is lower.
2. The method of claim 1 wherein the temperature is from room temperature to about 200° C.
3. The method of claim 2 wherein the ternary compound is regenerated by heating the compound to between 300° and 500° C.
4. The method of claim 3 wherein the ternary compound is heated to 500° C. at a pressure of about 10-7 Torr.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/337,339 US4397834A (en) | 1980-10-14 | 1982-01-06 | Method of gettering hydrogen under conditions of low pressure |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US19671080A | 1980-10-14 | 1980-10-14 | |
US06/337,339 US4397834A (en) | 1980-10-14 | 1982-01-06 | Method of gettering hydrogen under conditions of low pressure |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US19671080A Division | 1980-10-14 | 1980-10-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
US4397834A true US4397834A (en) | 1983-08-09 |
Family
ID=26892154
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US06/337,339 Expired - Fee Related US4397834A (en) | 1980-10-14 | 1982-01-06 | Method of gettering hydrogen under conditions of low pressure |
Country Status (1)
Country | Link |
---|---|
US (1) | US4397834A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4717551A (en) * | 1984-07-07 | 1988-01-05 | Daimler-Benz Aktiengesellschaft | Titanium-based alloy used as a gettering material |
WO2005032709A2 (en) * | 2003-09-30 | 2005-04-14 | General Electric Company | Hydrogen storage compositions and methods of manufacture thereof |
US20050098035A1 (en) * | 2003-11-06 | 2005-05-12 | Lemmon John P. | Devices and methods for hydrogen storage and generation |
EP1550634A2 (en) * | 2003-12-29 | 2005-07-06 | General Electric Company | Compositions and methods for hydrogen storage and recovery |
US20070014683A1 (en) * | 2003-09-30 | 2007-01-18 | General Electric Company | Hydrogen storage composition, and associated article and method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4163666A (en) * | 1978-01-31 | 1979-08-07 | Dan Davidov | Hydrogen charged alloys of Zr(A1-x Bx)2 and method of hydrogen storage |
-
1982
- 1982-01-06 US US06/337,339 patent/US4397834A/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4163666A (en) * | 1978-01-31 | 1979-08-07 | Dan Davidov | Hydrogen charged alloys of Zr(A1-x Bx)2 and method of hydrogen storage |
Non-Patent Citations (6)
Title |
---|
Nomura K., Ishido Y., Ono S., "A Novel Thermal Engine Using Metal Hydride", Energy Conversion, vol. 19, pp. 49 to 57, Oct. 13, 1978. * |
Pebler, A. et al., "Equilibrium Studies on the Systems ZrCr-H.sub.2 , ZrV.sub.2 -H.sub.2, and ZrMo.sub.2 -H.sub.2 between 0.degree. and 900.degree. C., Transactions of the Metallurgized Society of AIME, vol. 239 (10/67), pp. 1593-1600. * |
Pebler, A. et al., "Equilibrium Studies on the Systems ZrCr-H2 , ZrV2 -H2, and ZrMo2 -H2 between 0° and 900° C., Transactions of the Metallurgized Society of AIME, vol. 239 (10/67), pp. 1593-1600. |
Rohy, D. et al., "Electronic Specific Heat of Vanadium Chromium Hydride", Physical Review B, vol. 1, No. 6 (Mar. 15, 1970), pp. 2485-2487. * |
Van Mal, H. H. et al., "Hydrogen Absorption in LaNi.sub.5 and Related Compounds: Experimental Observations and their Explanation.", Journal of Less Common Metals, vol. 35 (1974), pp. 65-76. * |
Van Mal, H. H. et al., "Hydrogen Absorption in LaNi5 and Related Compounds: Experimental Observations and their Explanation.", Journal of Less Common Metals, vol. 35 (1974), pp. 65-76. |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4717551A (en) * | 1984-07-07 | 1988-01-05 | Daimler-Benz Aktiengesellschaft | Titanium-based alloy used as a gettering material |
WO2005032709A2 (en) * | 2003-09-30 | 2005-04-14 | General Electric Company | Hydrogen storage compositions and methods of manufacture thereof |
WO2005032709A3 (en) * | 2003-09-30 | 2005-08-11 | Gen Electric | Hydrogen storage compositions and methods of manufacture thereof |
US20070014683A1 (en) * | 2003-09-30 | 2007-01-18 | General Electric Company | Hydrogen storage composition, and associated article and method |
US20050098035A1 (en) * | 2003-11-06 | 2005-05-12 | Lemmon John P. | Devices and methods for hydrogen storage and generation |
US7029517B2 (en) | 2003-11-06 | 2006-04-18 | General Electric Company | Devices and methods for hydrogen storage and generation |
EP1550634A2 (en) * | 2003-12-29 | 2005-07-06 | General Electric Company | Compositions and methods for hydrogen storage and recovery |
US20050148466A1 (en) * | 2003-12-29 | 2005-07-07 | Lemmon John P. | Compositions and methods for hydrogen storage and recovery |
EP1550634A3 (en) * | 2003-12-29 | 2005-10-26 | General Electric Company | Compositions and methods for hydrogen storage and recovery |
US7175826B2 (en) | 2003-12-29 | 2007-02-13 | General Electric Company | Compositions and methods for hydrogen storage and recovery |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4360445A (en) | Oxygen stabilized zirconium-vanadium-iron alloy | |
US4668424A (en) | Low temperature reusable hydrogen getter | |
EP1817439B1 (en) | Non-evaporable getter alloys for hydrogen sorption | |
US4907948A (en) | Non-evaporable ternary gettering alloy, particularly for the sorption of water and water vapor in nuclear reactor fuel elements | |
US5180568A (en) | Recovery of tritium and deuterium from their oxides and intermetallic compound useful therein | |
CN108411182B (en) | Zr-Ti-Cr-V complex phase hydrogen storage alloy and preparation method thereof | |
Mizuno et al. | Titanium concentration in FeTix (l⩽ x⩽ 2) alloys and its effect on hydrogen storage properties | |
Boffito et al. | The properties of some zirconium-based gettering alloys for hydrogen isotope storage and purification | |
US4142300A (en) | Lanthanum nickel aluminum alloy | |
US4397834A (en) | Method of gettering hydrogen under conditions of low pressure | |
Boffito et al. | Equilibrium pressures of H2 and D2 for different getter materials and the effect of CO impurities | |
CN112226663B (en) | High-circulation-capacity ZrCo-based hydrogen isotope storage alloy and preparation and application thereof | |
US4743167A (en) | Devices for the sorption, storage and release of hydrogen isotopes | |
Meli et al. | XPS analysis of the getter mechanism and getter activation process | |
Doni et al. | Hydrogen isotope sorption and recovery by a nonevaporable getter combined with a chemical compressor material | |
CN112251647B (en) | ZrCo-based hydrogen isotope storage alloy with orthorhombic crystal structure and high cycle stability as well as preparation and application thereof | |
CN114672714A (en) | High-entropy hydrogen storage alloy and preparation method thereof | |
JPS5839218B2 (en) | Rare earth metal quaternary hydrogen storage alloy | |
Gruen et al. | Oxygen stabilized zirconium-vanadium-iron alloy | |
Ide et al. | Hydrogen isotope sorption properties of LaNi3Mn2 alloy as a candidate for the tritium storage material | |
JPS5950742B2 (en) | Titanium quaternary hydrogen storage alloy | |
JPS5939493B2 (en) | Titanium-cobalt multi-component hydrogen storage alloy | |
CN116240427A (en) | Getter alloy for purifying nitrogen and inert gas, and preparation and application thereof | |
JPH0613401B2 (en) | Method for producing metal hydride | |
Suzuki et al. | HYDRIDING BEHAVIORS OF Zr (FexMn1− x) 2 ALLOYS |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FEPP | Fee payment procedure |
Free format text: MAINTENANCE FEE REMINDER MAILED (ORIGINAL EVENT CODE: REM.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
LAPS | Lapse for failure to pay maintenance fees | ||
STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |
|
FP | Lapsed due to failure to pay maintenance fee |
Effective date: 19870809 |